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Drawing No. EH–FM–021 // Fluid Mechanics & Piping

Pump NPSH Calculator

Reviewed August 2026

Calculate NPSH available and margin for an open or pressurized suction source, including water vapour pressure from temperature.

Scope: Preliminary hydraulic screening. Use the pump manufacturer’s NPSHr curve and the project’s NPSH margin policy for final selection.

What problem does this solve?

Calculate net positive suction head available (NPSHa) and compare it with the pump manufacturer's NPSHr.

1. Set liquidTemperature determines vapour pressure.
2. Set pressureAtmospheric or vessel pressure acts on the liquid surface.
3. Describe suctionStatic level, pipe loss and inlet velocity reduce or increase head.
4. Compare marginNPSHa must exceed NPSHr with an appropriate project margin.

Inputs

Water vapour pressure is updated from temperature. Override for another liquid.

Results

Surface pressure head
Vapour pressure head
Velocity head
NPSH available
NPSH margin
Screening status
Important: NPSHr is normally determined by the pump manufacturer at a specified head-drop criterion. Cavitation risk also depends on suction energy, recirculation, air entrainment, operating point, fluid properties and margin policy.

Background

Engineering basis, assumptions, interpretation and practical limitations.

Frequently Asked Questions

Practical questions about NPSHa, NPSHr, suction head and cavitation margin.